JPH0321935Y2 - - Google Patents
Info
- Publication number
- JPH0321935Y2 JPH0321935Y2 JP1985126945U JP12694585U JPH0321935Y2 JP H0321935 Y2 JPH0321935 Y2 JP H0321935Y2 JP 1985126945 U JP1985126945 U JP 1985126945U JP 12694585 U JP12694585 U JP 12694585U JP H0321935 Y2 JPH0321935 Y2 JP H0321935Y2
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- hopper
- mixing
- granular
- raw materials
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000002994 raw material Substances 0.000 claims description 68
- 239000002985 plastic film Substances 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 6
- 238000004064 recycling Methods 0.000 claims description 5
- 229920006255 plastic film Polymers 0.000 claims description 3
- 238000010298 pulverizing process Methods 0.000 claims description 3
- 239000008187 granular material Substances 0.000 claims 1
- 239000010408 film Substances 0.000 description 5
- 239000004033 plastic Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/285—Feeding the extrusion material to the extruder
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/44—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with paddles or arms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/58—Component parts, details or accessories; Auxiliary operations
- B29B7/60—Component parts, details or accessories; Auxiliary operations for feeding, e.g. end guides for the incoming material
- B29B7/603—Component parts, details or accessories; Auxiliary operations for feeding, e.g. end guides for the incoming material in measured doses, e.g. proportioning of several materials
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Description
【考案の詳細な説明】
(産業上の利用分野)
本考案はプラスチツクシート・フイルム等の帯
状物を製造する際に発生する再生原料であるフラ
ツフと粒状原料の混合ホツパに関するものであ
る。[Detailed Description of the Invention] (Industrial Application Field) The present invention relates to a hopper for mixing flats and granular raw materials, which are recycled raw materials generated when manufacturing strips such as plastic sheets and films.
(従来の技術)
プラスチツクフイルム又はシート等の帯状物は
成形時に次に示すような製品外品が発生する。(Prior Art) When a plastic film or sheet is molded, the following off-product products are generated.
運転時に発生する未延伸部又は厚み不良部と
称する製品両側部(通常耳部と称する)の耳部
シート又はフイルム。 Edge sheet or film on both sides of the product (usually referred to as edges), which are called unstretched areas or areas with poor thickness that occur during operation.
スリツタでの切断時に発生する正規幅外品及
び厚み不揃い品等のスリツトロス品。 Slit loss products such as non-standard width products and uneven thickness products that occur when cutting with a sliver.
運転立上り時の非定常状態時に発生する製品
対象とならない製品外品。 Non-product items that are not applicable to products and occur during unsteady conditions at the start of operation.
運転時のフイルム又はシート等の破断品。 Broken film or sheet during operation.
これらの、いわゆる製品の対象外となるフイル
ム又はシートは再利用されるのが一般的であり、
比較的厚いシート又はフイルムは、クラツシヤー
等の粉砕機にて長辺が6〜8mm位の平板状に切断
される。これは一般にフラツフと呼ばれている。
また、非常に薄いフイルム類は、上記クラツシヤ
ー等による切断によると、嵩密度が小さく、搬送
上のトラブル発生の要因となるため、ペレツト化
されるケースが多い。このペレツト化は、再生用
プラスチツクを溶融して、溶融されたものを水中
又は空中で切断して得るもので、棒状(3mmφ×
3mm)、粒状(3mmφ球)又は板状(3mm×4mm)
の形状に作られる。 These so-called films or sheets that are not included in products are generally reused.
A relatively thick sheet or film is cut into flat plates with long sides of about 6 to 8 mm using a crusher such as a crusher. This is commonly called flats.
Furthermore, when very thin films are cut by the crusher or the like, their bulk density is low and this causes trouble during transportation, so they are often turned into pellets. This pelletization is obtained by melting recycled plastic and cutting the melt in water or in the air, and it is made into rod-shaped (3 mmφ
3mm), granular (3mmφ sphere) or plate (3mm x 4mm)
is made in the shape of
このうち、粉砕された再生用プラスチツク原料
(以下、再生粉砕原料という。)は、空送(圧送又
は吸引)によりホツパ本体内へ送られる。ペレツ
ト化され粒状品として再生された前記プラスチツ
ク原料又は新粒状プラスチツク原料(以下、粒状
原料という。)は、再生粉砕原料とは別個の搬送
ラインで、空送(圧送又は吸引)されて、前記ホ
ツパ本体内へ送られる。再生粉砕原料と、粒状原
料は、ホツパ本体内で混合される。 Among these, the pulverized plastic raw material for recycling (hereinafter referred to as recycled pulverized raw material) is sent into the hopper main body by air transport (pressure transport or suction). The plastic raw material or new granular plastic raw material (hereinafter referred to as granular raw material) that has been pelletized and recycled as a granular product is air-fed (pressure-fed or suctioned) to the hopper on a conveyance line separate from the recycled pulverized raw material. Sent into the main body. The recycled pulverized raw material and the granular raw material are mixed within the hopper body.
従来の混合方式の代表例を第2図及び第3図に
示す。 Representative examples of conventional mixing systems are shown in FIGS. 2 and 3.
まず第2図に示す従来のホツパについてその構
造を説明すると、1はホツパ本体を示し、該ホツ
パ本体1は円筒部に続く逆円錐部から構成され、
粒状及び再生粉砕原料を貯蔵、混合及び供給する
ためのものである。ホツパ本体1内にはアジテー
タ2が設置され、同アジテータ2は軸受11に回
転可能に支持された軸に螺旋状羽根が設けられた
もので、減速機5を介して駆動モータ4により回
転駆動されて粒状原料と再生粉砕原料を撹拌混合
し、図示せぬ押出機へ矢印A方向に供給するもの
である。 First, the structure of the conventional hopper shown in FIG. 2 will be explained. Reference numeral 1 indicates the hopper body, and the hopper body 1 is composed of a cylindrical part followed by an inverted conical part,
It is for storing, mixing and supplying granular and regrind raw materials. An agitator 2 is installed inside the hopper body 1, and the agitator 2 has a spiral blade provided on a shaft rotatably supported by a bearing 11, and is rotationally driven by a drive motor 4 via a reducer 5. The granular raw material and the regenerated pulverized raw material are stirred and mixed, and then supplied to an extruder (not shown) in the direction of arrow A.
ホツパ本体1の内壁所望の部位にはレベル計3
が設置されている。同レベル計3はホツパ本体1
内における原料の貯蔵量を検知して、その貯蔵量
を制御するものでパドル(羽根)式、静電方式等
によるものがある。 A level meter 3 is placed on the desired part of the inner wall of the hopper body 1.
is installed. The same level total 3 is Hoppa main body 1
There are paddle (blade) type, electrostatic type, and other types of devices that detect the amount of raw material stored in the tank and control the amount stored.
また、ホツパ本体1の上壁周面所望の部位には
再生粉砕原料8と粒状原料9の各投入口10,1
2が設けられ、夫々の投入口10,12はサイク
ロン6,7と連結されて、図示せぬフイルム粉砕
機及びペレツト製造装置から夫々空送(圧送又は
吸引)された再生粉砕原料8及び粒状原料9が
夫々のサイクロン6,7を通つて各投入口10,
12からホツパ本体1内に落下投入されるように
なつている。 In addition, each input port 10, 1 for the recycled pulverized raw material 8 and the granular raw material 9 is provided at a desired location on the upper wall circumferential surface of the hopper main body 1.
2 are provided, and respective input ports 10 and 12 are connected to cyclones 6 and 7, and regenerated pulverized raw materials 8 and granular raw materials are air-fed (pneumatically fed or sucked) from a film crusher and a pellet manufacturing device (not shown), respectively. 9 passes through the respective cyclones 6, 7 to each input port 10,
12 and are dropped into the hopper main body 1.
この第2図に示す方式では、別個の投入口1
0,12から投入された再生粉砕原料8と粒状原
料9が回転するアジテータ2により、撹拌、混合
され、矢印Aで示す様に図示せぬ押出機へ供給さ
れることになる。 In the system shown in FIG. 2, a separate input port 1
The regenerated pulverized raw material 8 and the granular raw material 9 introduced from 0 and 12 are stirred and mixed by the rotating agitator 2, and are supplied to an extruder (not shown) as shown by arrow A.
第3図に示す方式は再生粉砕原料用ホツパ13
と、同ホツパ13の外部に同心状に設けられた粒
状原料用ホツパ14を別個に設け、アジテータ2
の作用を受けるのは再生用粉砕原料8のみとし
て、再生粉砕原料用ホツパ13の下部にて、再生
粉砕原料8と粒状原料9を撹拌、混合し、第2図
で示したと同様に図示せぬ押出機へ供給するもの
である。 The system shown in Fig. 3 is a hopper 13 for regenerated pulverized raw materials.
A granular raw material hopper 14 is provided concentrically outside the hopper 13, and an agitator 2
Since only the regenerated pulverized raw material 8 is subjected to the action of the regenerated pulverized raw material 8, the regenerated pulverized raw material 8 and the granular raw material 9 are stirred and mixed at the lower part of the regenerated pulverized raw material hopper 13. It is supplied to the extruder.
ところで、第2図に示す混合ホツパにあつて
は、粉砕された再生粉砕原料の嵩密度は粒状原料
の嵩密度に比べて小さく(通常1/3〜1/10位)、ア
ジテータの羽根形状を工夫しても均等に混合され
にくく、押出機において、吐出変動が起こり易
く、最終的には製品の厚みむらとなり、製品とし
ての価置が低下したり或は製品外品となるという
不具合を生じるものであつた。 By the way, in the case of the mixing hopper shown in Fig. 2, the bulk density of the re-pulverized raw material is smaller than that of the granular raw material (usually about 1/3 to 1/10), so the shape of the agitator blades is No matter how much effort is made, it is difficult to mix evenly, and the extruder tends to fluctuate in discharge, which ultimately results in uneven product thickness, which lowers the value of the product or causes it to become a non-product. It was hot.
一方、第3図に示す混合ホツパは、上記不具合
を解消しようとして、再生粉砕原料と、粒状原料
の各専用ホツパ13,14と、その中心を同心上
として別個に設けて、嵩密度が低い再生粉砕原料
のみをアジテータ2をもつて撹拌し、再生粉砕原
料用ホツパ13の下部で、両者を混合して、押出
機へ供給するようにしたものであるが、両ホツパ
13,14の構造が複雑で、かつコスト高とな
り、また各ホツパ内の清掃に時間がかかる等の問
題点を有するものであつた。 On the other hand, the mixing hopper shown in FIG. 3 is designed to solve the above-mentioned problem by separately providing dedicated hoppers 13 and 14 for the recycled pulverized raw material and granular raw material, with their centers concentrically arranged, and the recycled hopper has a low bulk density. Only the pulverized raw material is agitated using the agitator 2, and both are mixed at the bottom of the hopper 13 for recycled pulverized raw material and supplied to the extruder, but the structure of both hoppers 13 and 14 is complicated. However, there are other problems, such as high cost and time-consuming cleaning inside each hopper.
(考案が解決しようとする問題点)
このように、従来のこの種混合ホツパにあつて
は再生粉砕原料と粒状原料が均等に混合されず、
吐出変動が発生し或は混合吐出が上手くいつても
構造が複雑でその取扱い及び保守が容易でない等
の問題点を有していた。(Problems to be solved by the invention) As described above, in the conventional mixing hopper of this kind, the recycled pulverized raw material and the granular raw material are not mixed evenly,
There have been problems such as discharge fluctuations occurring or even when mixing and discharging are successful, the structure is complex and handling and maintenance are not easy.
本考案はこれらの問題点を解決すべくなされた
もので、構造が簡単で、その取扱い及び保守が容
易であるにも拘わらず、均等な混合ができてその
吐出変動が少ない混合ホツパを提供しようとする
ものである。 The present invention was devised to solve these problems, and aims to provide a mixing hopper which is simple in structure, easy to handle and maintain, and which can mix evenly and has little variation in discharge. That is.
(問題点を解決するための手段)
このため、本考案はプラスチツクフイルム・シ
ート等の帯状物を成形する時に発生する製品外と
なる帯状物を粉砕した再生用原料と粒状原料を個
別に供給する投入口と、両原料を撹拌混合するア
ジテータを備えた混合用ホツパにおいて、嵩密度
の小さい前記粉砕された再生用原料の投入口を混
合ホツパ本体の上部に、また前記粒状原料の投入
口を混合ホツパ本体の下部逆円錐部に夫々設け、
両原料を混合ホツパ本体下部にて撹拌混合させる
ことを構成として、上記問題点を解決しようとす
るものである。(Means for solving the problem) For this reason, the present invention separately supplies raw materials for recycling and granular raw materials obtained by pulverizing strips that are outside the product and are generated during the molding of strips such as plastic films and sheets. In a mixing hopper equipped with an input port and an agitator for stirring and mixing both raw materials, the input port for the pulverized raw material for recycling having a small bulk density is placed at the top of the mixing hopper body, and the input port for the granular raw material is placed at the top of the mixing hopper body. Each is provided in the lower inverted conical part of the hopper body,
The above-mentioned problems are attempted to be solved by stirring and mixing both raw materials at the lower part of the mixing hopper body.
(作用)
帯状物の粉砕した再生粉砕原料を上部から、粒
状原料を下部側面から同一混合ホツパ内へ投入さ
せ、その下部にてアジテータの作用により両者を
混合して、押出機へ供給する。(Operation) The regenerated pulverized raw material obtained by pulverizing the strip is introduced into the same mixing hopper from the upper part, and the granular raw material is introduced into the same mixing hopper from the lower side, and both are mixed by the action of the agitator at the lower part and then supplied to the extruder.
(実施例)
以下、本考案の実施例を第1図に基づいて説明
する。(Example) Hereinafter, an example of the present invention will be described based on FIG. 1.
なお、同図中第2図及び第3図で示した従来の
混合ホツパと同一符号を付してある部分は本実施
例にあつても同一部分を示すものであるので、以
下従来との相違点を中心に説明する。 In addition, in this figure, the parts with the same reference numerals as those in the conventional mixing hopper shown in FIGS. 2 and 3 refer to the same parts in this embodiment, so the differences from the conventional mixing hopper will be explained below. I will mainly explain the points.
図中20は粒状原料投入口であつて、ホツパ本
体の逆円錐部21に傾斜させて設けられ、同円錐
部の下部に向けて粒状原料9を積極的に供給す
る。 In the figure, reference numeral 20 denotes a granular raw material input port, which is provided at an angle to an inverted conical portion 21 of the hopper body, and actively supplies the granular raw material 9 toward the lower part of the conical portion.
ここで、再生粉砕原料8の投入口10は第2図
で示した従来のホツパと同様にホツパ本体1の上
面周縁部に設けられる。 Here, the input port 10 for the regenerated pulverized raw material 8 is provided at the upper peripheral edge of the hopper main body 1, similar to the conventional hopper shown in FIG.
また、アジテータ22も第2図に示したものと
同様ではあるが、本実施例にあつてはホツパ本体
1の逆円錐部21に設けられた前記粒状原料投入
口から供給される粒状原料に対しても撹拌作用を
与えるために、ホツパ本体1の円錐面に沿つて存
在するバー22aを付設している。ここに示すも
のは一例であつて他の適当な構造とすることも勿
論可能なものである。 Further, the agitator 22 is also similar to the one shown in FIG. A bar 22a is provided along the conical surface of the hopper body 1 in order to provide stirring action. What is shown here is an example, and other suitable structures are of course possible.
このアジテータ22によつて再生粉砕原料8を
撹拌しつつ、ホツパ本体1の下部へ供給して、前
記粒状原料投入口20から投入される粒状原料9
と十分に撹拌及び混練させることになる。 The regenerated pulverized raw material 8 is agitated by the agitator 22 and supplied to the lower part of the hopper main body 1, and the granular raw material 9 is inputted from the granular raw material input port 20.
Thoroughly stir and knead.
次にその作用について述べると、図示しない粉
砕機から矢印Bの様に空送されてきた再生粉砕原
料8はサイクロン6を介してホツパ本体1へ投入
される。ここで、粉砕原料8の混合比率は、アジ
テータ22の回転数を制御することにより自由に
変更できる。 Next, the operation will be described. Regenerated pulverized raw material 8, which has been air-fed from a not-shown pulverizer as shown by arrow B, is fed into the hopper body 1 via the cyclone 6. Here, the mixing ratio of the pulverized raw material 8 can be freely changed by controlling the rotation speed of the agitator 22.
一方、図示しないペレツト製造装置から矢印C
の様に空送されてきた粒状原料9はサイクロン7
を介して空気と分別され、粒状原料投入口20か
らアジテータ22の下部へ投入される。 On the other hand, from the pellet manufacturing device (not shown)
The granular raw material 9 that has been air-fed like this is transferred to the cyclone 7.
The granular raw material is separated from air through the granular raw material input port 20 and is input into the lower part of the agitator 22.
再生粉砕原料8はアジテータ22により、撹拌
されつつホツパ本体1の下部へ導かれ、粒状原料
投入口20からの粒状原料9とともに十分に撹
拌・混練されて図示せぬ押出機へ供給される。 The regenerated pulverized raw material 8 is guided to the lower part of the hopper body 1 while being stirred by the agitator 22, and is thoroughly stirred and kneaded together with the granular raw material 9 from the granular raw material input port 20, and then supplied to an extruder (not shown).
(考案の効果)
以上、詳細に説明した如く、本考案によると粒
状原料と粉砕原料を単体の混合ホツパをもつて、
均一に混合と供給をすることが可能となり高品質
の製品を生産できる上に、ホツパ本体の構造が単
純化されているためホツパ内の清掃作業その他の
保守管理を効率的に行うことができるものであ
る。(Effects of the invention) As explained above in detail, according to the invention, granular raw materials and pulverized raw materials are mixed with a single mixing hopper,
Not only is it possible to mix and feed evenly, producing high-quality products, but the structure of the hopper body is simplified, so cleaning work and other maintenance inside the hopper can be carried out efficiently. It is.
第1図は本考案の実施例を示す混合ホツパの断
面図、第2図は従来の混合ホツパの一例を示す断
面図、第3図は従来の他例を示す混合ホツパの断
面図である。
図の主要部分の説明、1……ホツパ本体、8…
…再生粉砕原料、9……粒状(プラスチツク)原
料、10……再生粉砕原料投入口、20……粒状
原料投入口、21……逆円錐部、22……アジテ
ータ。
FIG. 1 is a cross-sectional view of a mixing hopper showing an embodiment of the present invention, FIG. 2 is a cross-sectional view of an example of a conventional mixing hopper, and FIG. 3 is a cross-sectional view of another conventional mixing hopper. Explanation of the main parts of the figure, 1... hopper body, 8...
...Regenerated pulverized raw material, 9... Granular (plastic) raw material, 10... Regenerated pulverized raw material inlet, 20... Granular raw material inlet, 21... Inverted conical part, 22... Agitator.
Claims (1)
形する時に発生する製品外となる帯状物を粉砕し
た再生用原料と粒状原料を個別に供給する投入口
と、両原料を撹拌混合するアジテータを備えた混
合用ホツパにおいて、嵩密度の小さい前記粉砕さ
れた再生用原料の投入口を混合ホツパ本体の上部
に、また前記粒状原料の投入口を混合ホツパ本体
の下部逆円錐部に夫々設け、両原料を混合ホツパ
本体下部にて撹拌混合させることを特徴とする混
合ホツパ。 For mixing, equipped with an input port for separately supplying raw materials for recycling and granular raw materials, which are obtained by pulverizing the strips that are generated when forming strips of plastic film and sheets, etc., that are outside of the product, and an agitator that stirs and mixes both raw materials. In the hopper, an input port for the pulverized raw material for recycling having a small bulk density is provided in the upper part of the mixing hopper body, and an input port for the granular material is provided in the lower inverted conical part of the mixing hopper body, and both raw materials are fed into the mixing hopper. A mixing hopper characterized by stirring and mixing at the bottom of the main body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1985126945U JPH0321935Y2 (en) | 1985-08-20 | 1985-08-20 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1985126945U JPH0321935Y2 (en) | 1985-08-20 | 1985-08-20 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6235806U JPS6235806U (en) | 1987-03-03 |
| JPH0321935Y2 true JPH0321935Y2 (en) | 1991-05-14 |
Family
ID=31021226
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1985126945U Expired JPH0321935Y2 (en) | 1985-08-20 | 1985-08-20 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0321935Y2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2510499Y2 (en) * | 1993-04-27 | 1996-09-11 | 博之 清水 | Concrete mold for hole forming |
| JP2529639B2 (en) * | 1993-04-27 | 1996-08-28 | 博之 清水 | Slave mounting method for concrete formwork |
| CN106426613B (en) * | 2016-08-26 | 2019-01-18 | 太仓市鸿运包装材料有限公司 | One kind can quantity-produced multilayer agitating device and its working method |
-
1985
- 1985-08-20 JP JP1985126945U patent/JPH0321935Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6235806U (en) | 1987-03-03 |
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